Enrichment Method of Ergosterol Peroxide from Sporoderm-Broken Ganoderma Lucidum Spore Powder

ABSTRACT

The invention provides an enrichment method of Ergosterol peroxide from sporoderm-broken  Ganoderma lucidum  spore powder, comprising the steps of preparing crude extract containing Ergosterol peroxide, purification by medium pressure preparative chromatography, purification by simulated moving-bed, and recrystallization. The operation of this invention is simple and stable, with higher yield and low cost, suiting for industrial continuous production.

TECHNICAL FIELD

This invention relates to an enrichment method of Ergosterol peroxide, in particular to an enrichment method of Ergosterol peroxide from sporoderm-broken Ganoderma lucidum spore powder, belonging to the field of extraction-separation.

BACKGROUND

Ergosterol peroxide, with the full name of 5α,8α-Epidioxyergosta-6,22-dien-3β-ol, is known compounds, belonging to the sterols, widely existing in edible-medicinal fungus or other fungus. There are many reports about its activities, for example, the patent, application No. 201410311586.3, disclosed that it has synergy with taxol in killing or damaging Hela cancer cells, reducing chemotherapy's side effects and cost by reducing dosage of taxol. The patent, of which application No. is 200610126091.9, disclosed that ergosterol peroxide has significant anti-tumor (human breast cancer and liver cancer) pharmacology activity, and has no harmful effects on immune organs and the weight; The patent, of which application No. is 201210233192.1, reported that it has significant inhibitory effect on malignant breast cancer cells (MT-1), lymphoma cancer cells (Jurkat) and brain tumor cells (U87), and has killing effect on brain tumor stem cells, which are drug-resistant tumor stem cells; The patent, of which application No. is 200810119948.3, reported that ergosterol peroxide has remarkable antifungal bioactivity, and can be used in the field of natural antibiotic; The patent, of which application No. is 01817014.5, disclosed that ergosterol peroxide has strong inhibitory effects on the formation of melanin, and can be used in the field of whitening cosmetics; The patent, of which application No. is 01817014.5, disclosed that it has poisoning effects on agricultural pests, such as pieris rapae, prodenia litura, aphid and so on, therefore can be used in the field of pesticide. In addition, ergosterol peroxide reported in the other literature that it has extensive pharmacological actions, such as antioxidation, antituberculosis, anti-inflammation, anti-atherosclerosis, inhibiting the proliferation of T-cells, and so on.

There are fewer reports on the methods of extraction, separation and purification of ergosterol peroxide, which was identified from isolated unknown monomer in the most of reports, and there are still cases misjudged by the author in a fraction of these reports. The patent, of which the application No. is 201210233192.1, broke the sporoderm of Ganoderma lucidum spore powder by the enzyme method and obtained the extract by supercritical carbon dioxide extraction method. Tracing the activity with the tumor inhibitory rate, a single monomer with highest activity, which was identified as ergosterol peroxide, was obtained by three times positive silica gel column chromatography with chloroform, ethyl acetate, petroleum ether-ethyl acetate as eluent in sequence, and followed by preparative chromatography. Using Naematoloma fasciculare fruit body and mycelium as material, The patent, of which the application No. is 201210233192.1 obtained two monomers by extracting with methyl alcohol and petroleum ether in turn, positive silica gel column chromatography with cyclohexane-ethyl acetate as eluent, and recrystallizing for several times; One of the monomers was identified as ergosterol peroxide. In the patent of which application No. is 200810119948.3, a petroleum ether fraction from fermented liquid of fungus Ppf4, and another petroleum ether fraction from the acetone extract of hypha, were merged; three monomers were obtained by positive silica gel column chromatography with cyclohexane-acetone as eluent, followed by gel column and reversed silica gel column chromatography; One of the monomers was identified as ergosterol peroxide. Using the fruit body of Ganoderma lucidum as material, Cheng Chunru (“Chemical constituents from the fruiting body of Ganoderma lucidum with cytotoxicity investigations”, Journal of Shenyang Pharmaceutical University, 2014, 31(2): 102-106.) obtained a fraction by extraction with 95% ethanol, extraction with petroleum ether, positive silica gel column chromatography with petroleum ether-ethyl acetate as eluent; removing a monomer with recrystallization, another monomer was obtained finally by semi-preparative isolation from the mother liquo and identified as ergosterol peroxide. Using Shiraia bambusicola as material, Liu Yafeng, et al. (“Separation of peroxy-ergosterol in fungus” Zhuhuang, Journal of Tianjin University of Traditional Chinese Medicine, 2004, 23(1): 15-16.) obtained a monomer, which was identified as ergosterol peroxide, by extraction with ethyl acetate and positive silica gel column chromatography for several times. Zhang Nengsheng et al. (“Isolation and Purification of Peroxy-ergosterol from Paecilomyces fumosoroseus by High-Speed-Counter-Current Chromatography and identification by ESI-MS”, Food and Fermentation Industries, 2009, 35(6): 14-16.) studied the isolation and purification of peroxy-ergosterol from paecilomyces fumosoroseus by advanced high-speed-counter-current chromatography, but the obtained target product is actually not peroxy-ergosterol, because that peroxy-ergosterol has no UV absorption at 240-400 nm, while 280 nm was used as UV absorption wavelength to detect the process of isolation and to test the purity in this reports, and the chromatogram showed a larger absorbency. So that may be a miscarriage from the author.

The above-mentioned techniques of separation and purification of ergosterol peroxide have something in common: extraction with neutral or strong polarity organic solvent at first, then removing impurities by extraction for several times with Weak polarity organic solvent, followed by positive silica gel column chromatography for several times repeatedly with weak polarity organic solvent having a certain ratio as eluent, collecting the target fractions, and then obtaining the monomer of ergosterol peroxide by the steps of gel chromatography, preparative chromatography, recrytallization and so on; the yields of ergosterol peroxide are mostly in the grade of milligram, and the processes started mostly from the unknown, that is to say, the monomer was obtained at first, and then was identified as ergosterol peroxide; the purposes of preparation were to elucidate the chemical composition of natural plants and fungus, the processes of preparation belong to fumbling isolation, the processes are complex and varied without considering the cost and yield, and the whole processes of preparation used toxic and volatile reagents without considering environmental safety. In summary, the above mentioned techniques are not suitable for direct application in industrial production.

The simulated moving bed chromatography separation system is the organic combination of simulated moving-bed technology and chromatographic separation technology. Chromatographic columns in series connection are adopted, and continuous switchover between the inlet and outlet can be achieved by electromagnetic valve in the system, so the efficiency of moving-bed is simulated, in which the stationary phase circulates with continuous countercurrent. The combination of simulated moving-bed and chromatography changed chromatographic separation from discontinuous into continuous process, having the characteristics of large output, high yield, and high purity, and has been applied in the field of petroleum and chemicals, food, fermentation, medicine and so on, mainly in the purification of petrochemicals, saccharide, fermented product, active components in traditional Chinese medicine, and chiral compounds. But there is no report about purification of ergosterol peroxide by using simulated moving-bed technology.

CONTENTS OF THE INVENTION

Aiming at the drawbacks of the prior art, the object of this invention is to provide an enrichment method of Ergosterol peroxide from sporoderm-broken Ganoderma lucidum spore powder, which has a simple and stable operation, higher yield and low cost, suiting for industrial continuous production.

In order to achieve the above mentioned objects, the technical solutions of this invention are as follows:

An enrichment method of Ergosterol peroxide from sporoderm-broken Ganoderma lucidum spore powder comprising the following steps:

(1) Preparing crude extract containing Ergosterol peroxide: taking the sporoderm-broken Ganoderma lucidum spore powder, performing extraction by percolation or reflux method, concentrating the extract liquid to dryness under reduced pressure, and obtaining the crude extract A containing Ergosterol peroxide;

(2) Purification by medium pressure preparative chromatography: dissolving the crude extract A containing Ergosterol peroxide prepared in the step (1) with 60-95% methanol aqueous solution to obtain the sample solution for medium pressure preparative chromatography, performing purification by medium pressure preparative chromatography, collecting the fraction containing Ergosterol peroxide, concentrating it to dryness under reduced pressure to obtain the extractum B containing Ergosterol peroxide;

(3) Purification by simulated moving-bed: dissolving the extractum B containing Ergosterol peroxide prepared in the step (2) with 60-95% methanol aqueous solution to obtain the sample solution, injecting the sample solution into the simulated moving-bed chromatography separation system for further purification, concentrating the extract liquor containing Ergosterol peroxide to dryness under reduced pressure, and obtaining the dry extract C rich in Ergosterol peroxide;

(4) Dissolving the dry extract C rich in Ergosterol peroxide prepared in the step (3) with ethyl acetate-cyclohexane under heating conditions, transferring it into a environment at a temperature of 0-8° C. for recrystallization, filtering and washing the precipitate to obtain Ergosterol peroxide with high purity.

The extraction solvent of percolation or reflux method said in step (1) is one of ethyl acetate, cyclohexane and petroleum ether, or a mixture of them with any ratio.

The said percolation in step (1), wherein, the immersing time is 24-48 h, the immersing temperature is room temperature, and percolate is collected at approximate constant speed for 5-10 BV.

The said reflux method in step (1), wherein, the liquid-solid ratio is 6-10, the extracting time at boiling condition is 1-2 h, the residue is repeatedly extracted for 1-2 times, and the filtrate is merged.

The said step (2), wherein, the medium pressure preparative chromatography column is packed with 30-50 μm ODS silica gel, the height of column is 45 cm, the solid content of sample solution is 0.05-0.2 g/mL, the injection rate is 2-5 mL/min and the injection volume is 0.1 BV, performing isocratic elution with 60-95% methanol aqueous solution at the rate of 1.2-2.0 BV/h.

The said step (3), wherein, the solid content of sample solution is 0.05-0.2 g/mL, the simulated moving-bed chromatography system uses ODS reversed silica gel with particle size of 30-50 μm as packing materials, the system, adopting 8-16 columns in series connection, is divided into four areas, each of which having 2-4 columns in series connection, the system parameters are set up as follows: room temperature, flow rate of injection pump is 3-6 mL/min, flow rate of elution pump is 16-38 mL/min, Extraction velocity is 10-23 mL/min, flow rate for raffinate is 9-21mL/min, and switching time is 10-24 min.

The said step (4), wherein, the dosage of ethyl acetate-cyclohexane is 10-20 times that of the dry extract C, the volume ratio of ethyl acetate to cyclohexane is 50:50-10:90, and the time of recrystallization is 36-48 h.

Compared with the extract methods of ergosterol peroxide in prior art, the present invention has the advantages of:

(1) The medium pressure preparative chromatography in this invention play a function of removing impurities and enrichment, compared with the existing processes (extraction for several times with low polarity organic solvents or preliminary separation with positive silica gel chromatography), having no new impurities and toxic or harmful substances introduced, maintaining the natural quality of ergosterol peroxide well, and being good and safe for the environment. Both the yield and content of ergosterol peroxide in the obtained extractum are higher, due to the better effects in removing impurities. In addition, removing impurities more fully and thoroughly in this invention can remove almost all of impurities, whose polarity is lower than ergosterol peroxide. Therefore it is more suitable for being pretreatment of the enrichment process by simulated moving-bed chromatography.

(2) The present invention performs further purification by simulated moving-bed chromatography. The combination of simulated moving-bed and chromatography changed chromatographic separation from discontinuous into continuous process, and retains the advantages of chromatographic separation, such as excellent separation efficiency, low-energy, low-material consumption, operation at room temperature and so on. The stationary phase and mobile phase can be repeatedly applied, the efficiency is raised greatly, and the cost is reduced, due to the simulated countercurrent. Simulated moving-bed chromatography, in which the fractions are acquired from the beginning and end of the bands, makes the extract process easily controlled; the separation capability is enhanced and the yield is increased, due to introducing rectification and reflux system; the productivity is increased, the automation level and efficiency are enhanced, the solvent wastage is reduced, and the production environment is improved greatly, due to introducing continuous system.

(3) The purity of ergosterol peroxide, obtained by primary extraction, purification with medium pressure preparative chromatography, and enrichment with simulated moving-bed chromatography, is 50-80% in the present invention, which is higher.

EXAMPLES

The examples below further illustrate the invention, rather than limiting the scope thereof. The related methods and materials in this invention are separately the conventional methods and materials available in the market, unless specially stated otherwise.

Example 1

Acquiring ergosterol peroxide from sporoderm-broken Ganoderma lucidum spore powder by following steps:

(1) Preparing crude extract containing Ergosterol peroxide: taking the sporoderm-broken Ganoderma lucidum spore powder, performing extraction by percolation, of which the extraction solvent is ethyl acetate, the immersing time is 40 h at room temperature, percolate is collected at approximate constant speed for 8 BV; concentrating the extract liquid to dryness under reduced pressure by rotary evaporator, the bathing temperature at 65° C., and the vacuum degree below −0.085, and obtaining the crude extract A with an ergosterol peroxide content of 0.62% revealed by the test results.

(2) Purification by medium pressure preparative chromatography: dissolving the crude extract A containing Ergosterol peroxide prepared in the step (1) with 60% methanol aqueous solution by heating and ultrasonic, filtrating the solution with 0.45 μm millipore filter to obtain the sample solution for medium pressure preparative chromatography, of which the solid content is 0.05 g/mL; performing purification by medium pressure preparative chromatography, of which the medium pressure preparative chromatography column is packed with 50 μm ODS silica gel, the height of column is 45 cm, the injection rate is 2 mL/min, and the injection volume is 0.1 BV, performing isocratic elution with 60% methanol aqueous solution at the rate of 1.2 BV/h; collecting the fraction containing Ergosterol peroxide, concentrating it to dryness under reduced pressure by rotary evaporator, the bathing temperature at 70° C., and the vacuum degree below −0.085, to obtain the extractum B with an Ergosterol peroxide content of 16.8%. In this step, the impurities with low polarity are removed almost, and the impurities with high polarity are partly removed.

(3) Purification by simulated moving-bed: simulated moving bed chromatography separation system includes elution pump, injection pump, extracting pump, chromatographic columns, electromagnetic valve, check valve, signal collector, system controller, and so on, thereinto, the flow rate of both elution pump and extracting pump are 0-250 mL/min, that of injection pump is 0-50 mL/min, the operating pressures and operating temperatures of the three pumps are respectively 0-10 MPa and 15-35° C. The system, using ODS reversed silica gel with particle size of 30 um as packing materials, adopting 16 columns in series connection, is divided into four areas, each of which having 4 columns in series connection. The positions of inlet and outlet can be changed at intervals by switchover according to the electromagnetic valve, thus simulated moving of the separated bed is achieved. Dissolving the extractum B containing Ergosterol peroxide prepared in the step (2) with 95% methanol aqueous solution by heating and ultrasonic, filtrating the solution with 0.45 μm millipore filter to obtain the sample solution, of which the solid content is 0.2 g/mL; injecting the sample solution into the simulated moving-bed chromatography separation system for further purification; The system parameters are set up as follows: room temperature, flow rate of injection pump is 3 mL/min, flow rate of elution pump is 16 mL/min, is 10 mL/min, flow rate of raffinate is 9 mL/min, and switching time is 24 min; concentrating the extract liquor containing Ergosterol peroxide to dryness under reduced pressure by rotary evaporator, the bathing temperature at 70° C., and the vacuum degree below −0.085, to obtain the dry extract C rich in Ergosterol peroxide.

(4) Dissolving the dry extract C rich in Ergosterol peroxide prepared in the step (3) with ethyl acetate-cyclohexane under heating conditions, transferring it into an environment at a temperature of 0° C. for recrystallization, filtering and washing the precipitate to obtain Ergosterol peroxide with a purity of 53.7%. In this step, the dosage of ethyl acetate-cyclohexane is 20 times that of the dry extract C, the volume ratio of ethyl acetate to cyclohexane is 10:90, and the time of recrystallization is 40 h.

In this example, the content of Ergosterol peroxide is tested by HPLC-ESLD, and the chromatographic conditions are as follows: Agilent 1200 Series High Performance Liquid Chromatography (HPLC) System, Chromachem evaporative light-scattering detector (ELSD) from ESA company in America, Waters Symmetry Shield RP18 columns (4.6×250 mm, 5 μm), 90% acetonitrile aqueous solution as the mobile phase, isocratic elution, flow rate: 0.8mL/min, column temperature: 30° C., temperature of drift tube: 80° C., temperature of atomizer: 60° C., nitrogen pressure: 25 psi, gain: 3, injection volume: 20 μL, purity calculation by external standard method.

Example 2

Acquiring ergosterol peroxide from sporoderm-broken Ganoderma lucidum spore powder by following steps:

(1) Preparing crude extract containing Ergosterol peroxide: taking the sporoderm-broken Ganoderma lucidum spore powder, performing extraction by reflux method, of which the extraction solvent is cyclohexane-petroleum ether (1:1), the liquid-solid ratio is 10, the extracting time at boiling condition is 2 h, the residue is repeatedly extracted for once, and the filtrate is merged; concentrating the extract liquid to dryness under reduced pressure by rotary evaporator, the bathing temperature at 60° C., and the vacuum degree below −0.085, and obtaining the crude extract A with an ergosterol peroxide content of 0.98% revealed by the test results.

(2) Purification by medium pressure preparative chromatography: dissolving the crude extract A containing Ergosterol peroxide prepared in the step (1) with 95% methanol aqueous solution by heating and ultrasonic, filtrating the solution with 0.45 μm millipore filter to obtain the sample solution for medium pressure preparative chromatography, of which the solid content is 0.2 g/mL; performing purification by medium pressure preparative chromatography, of which the medium pressure preparative chromatography column is packed with 30 μm ODS silica gel, the height of column is 45 cm, the injection rate is 5 mL/min, and the injection volume is 0.1 BV, performing isocratic elution with 80% methanol aqueous solution at the rate of 2.0 BV/h; collecting the fraction containing Ergosterol peroxide, concentrating it to dryness under reduced pressure by rotary evaporator, the bathing temperature at 65° C., and the vacuum degree below −0.085, to obtain the extractum B with an Ergosterol peroxide content of 10.2%. In this step, the impurities with low polarity are removed almost, and the impurities with high polarity are partly removed.

(3) Purification by simulated moving-bed: simulated moving bed chromatography separation system includes elution pump, injection pump, extracting pump, chromatographic columns, electromagnetic valve, check valve, signal collector, system controller, and so on, thereinto, the flow rate of both elution pump and extracting pump are 0-250 mL/min, that of injection pump is 0-50 mL/min, the operating pressures and operating temperatures of the three pumps are respectively 0-10 MPa and 15-35° C. The system, using ODS reversed silica gel with particle size of 50 μm as packing materials, adopting 8 columns in series connection, is divided into four areas, each of which having 2 columns in series connection. The positions of inlet and outlet can be changed at intervals by switchover according to the electromagnetic valve, thus simulated moving of the separated bed is achieved. Dissolving the extractum B containing Ergosterol peroxide prepared in the step (2) with 60% methanol aqueous solution by heating and ultrasonic, filtrating the solution with 0.45 μm millipore filter to obtain the sample solution, of which the solid content is 0.05 g/mL; injecting the sample solution into the simulated moving-bed chromatography separation system for further purification; The system parameters are set up as follows: room temperature, flow rate of injection pump is 6 mL/min, flow rate of elution pump is 38 mL/min, Extraction velocity is 23 mL/min, flow rate of raffinate is 21 mL/min, and switching time is 10 min; concentrating the extract liquor containing Ergosterol peroxide to dryness under reduced pressure by rotary evaporator, the bathing temperature at 65° C., and the vacuum degree below −0.085, to obtain the dry extract C rich in Ergosterol peroxide.

(4) Dissolving the dry extract C rich in Ergosterol peroxide prepared in the step (3) with ethyl acetate-cyclohexane under heating conditions, transferring it into a environment at a temperature of 8° C. for recrystallization, filtering and washing the precipitate to obtain Ergosterol peroxide with a purity of 66.3%. In this step, the dosage of ethyl acetate-cyclohexane is 10 times that of the dry extract C, the volume ratio of ethyl acetate to cyclohexane is 50:50, and the time of recrystallization is 48 h.

In this example, the method testing the content of Ergosterol peroxide is the same as that in the example 1.

Example 3

Acquiring ergosterol peroxide from sporoderm-broken Ganoderma lucidum spore powder by following steps:

(1) Preparing crude extract containing Ergosterol peroxide: taking the sporoderm-broken Ganoderma lucidum spore powder, performing extraction by reflux method, of which the extraction solvent is ethyl acetate-cyclohexane (1:1), the liquid-solid ratio is 6, the extracting time at boiling condition is 1 h, the residue is repeatedly extracted for twice, and the filtrate is merged; concentrating the extract liquid to dryness under reduced pressure by rotary evaporator, the bathing temperature at 70° C., and the vacuum degree below −0.085, and obtaining the crude extract A with an ergosterol peroxide content of 1.23% revealed by the test results.

(2) Purification by medium pressure preparative chromatography: dissolving the crude extract A containing Ergosterol peroxide prepared in the step (1) with 80% methanol aqueous solution by heating and ultrasonic, filtrating the solution with 0.45 μm millipore filter to obtain the sample solution for medium pressure preparative chromatography, of which the solid content is 0.15 g/mL;

performing purification by medium pressure preparative chromatography, of which the medium pressure preparative chromatography column is packed with 40 μm ODS silica gel, the height of column is 45 cm, the injection rate is 4 mL/min, and the injection volume is 0.1 BV, performing isocratic elution with 80% methanol aqueous solution at the rate of 1.8 BV/h; collecting the fraction containing Ergosterol peroxide, concentrating it to dryness under reduced pressure by rotary evaporator, the bathing temperature at 60° C., and the vacuum degree below −0.085, to obtain the extractum B with an Ergosterol peroxide content of 20.4%. In this step, the impurities with low polarity are removed almost, and the impurities with high polarity are partly removed.

(3) Purification by simulated moving-bed: simulated moving bed chromatography separation system includes elution pump, injection pump, extracting pump, chromatographic columns, electromagnetic valve, check valve, signal collector, system controller, and so on, thereinto, the flow rate of both elution pump and extracting pump are 0-250 mL/min, that of injection pump is 0-50 mL/min, the operating pressures and operating temperatures of the three pumps are respectively 0-10 MPa and 15-35° C. The system, using ODS reversed silica gel with particle size of 40 μm as packing materials, adopting 12 columns in series connection, is divided into four areas, each of which having 3 columns in series connection. The positions of inlet and outlet can be changed at intervals by switchover according to the electromagnetic valve, thus simulated moving of the separated bed is achieved. Dissolving the extractum B containing Ergosterol peroxide prepared in the step (2) with 85% methanol aqueous solution by heating and ultrasonic, filtrating the solution with 0.45 μm millipore filter to obtain the sample solution, of which the solid content is 0.15 g/mL; injecting the sample solution into the simulated moving-bed chromatography separation system for further purification; The system parameters are set up as follows: room temperature, flow rate of injection pump is 5 mL/min, flow rate of elution pump is 33 mL/min, Extraction velocity is 20 mL/min, flow rate of raffinate is 18 mL/min, and switching time is 15 min; concentrating the extract liquor containing Ergosterol peroxide to dryness under reduced pressure by rotary evaporator, the bathing temperature at 60° C., and the vacuum degree below −0.085, to obtain the dry extract C rich in Ergosterol peroxide.

(4) Dissolving the dry extract C rich in Ergosterol peroxide prepared in the step (3) with ethyl acetate-cyclohexane under heating conditions, transferring it into a environment at a temperature of 4° C. for recrystallization, filtering and washing the precipitate to obtain Ergosterol peroxide with a purity of 79.63%. In this step, the dosage of ethyl acetate-cyclohexane is 15 times that of the dry extract C, the volume ratio of ethyl acetate to cyclohexane is 30:70, and the time of recrystallization is 36 h.

In this example, the method testing the content of Ergosterol peroxide is the same as that in the example 1.

The above are only preferred embodiments of the present disclosure and should not be used for limiting the present disclosure. For those skilled in the art, any modifications, equivalent replacements, improvements and the like within the spirit and principle of the present disclosure shall fall within the scope of protection of the present disclosure. 

1. An enrichment method of Ergosterol peroxide from sporoderm-broken Ganoderma lucidum spore powder, comprising the following steps: (1) Preparing crude extract containing Ergosterol peroxide: taking the sporoderm-broken Ganoderma lucidum spore powder, performing extraction by percolation or reflux method, concentrating the extract liquid to dryness under reduced pressure, and obtaining the crude extract A containing Ergosterol peroxide; (2) Purification by medium pressure preparative chromatography: dissolving the crude extract A containing Ergosterol peroxide prepared in the step (1) with 60-95% methanol aqueous solution to obtain the sample solution for medium pressure preparative chromatography, performing purification by medium pressure preparative chromatography, collecting the fraction containing Ergosterol peroxide, concentrating it to dryness under reduced pressure to obtain the extractum B containing Ergosterol peroxide; (3) Purification by simulated moving-bed: dissolving the extractum B containing Ergosterol peroxide prepared in the step (2) with 60-95% methanol aqueous solution to obtain the sample solution, injecting the sample solution into the simulated moving-bed chromatography separation system for further purification, concentrating the extract liquor containing Ergosterol peroxide to dryness under reduced pressure, and obtaining the dry extract C rich in Ergosterol peroxide; (4) Dissolving the dry extract C rich in Ergosterol peroxide prepared in the step (3) with ethyl acetate-cyclohexane under heating conditions, transferring it into a environment at a temperature of 0-8° C. for recrystallization, filtering and washing the precipitate to obtain Ergosterol peroxide with high purity.
 2. Enrichment method of Ergosterol peroxide from sporoderm-broken Ganoderma lucidum spore powder according to claim 1, characterized in that the extraction solvent of percolation or reflux method said in step (1) is one of ethyl acetate, cyclohexane and petroleum, or a mixture of them with any ratio.
 3. Enrichment method of Ergosterol peroxide from sporoderm-broken Ganoderma lucidum spore powder according to claim 2, characterized in that the said percolation in step (1), wherein, the immersing time is 24-48 h, the immersing temperature is room temperature, and percolate is collected at approximate constant speed for 5-10 BV.
 4. Enrichment method of Ergosterol peroxide from sporoderm-broken Ganoderma lucidum spore powder according to claim 2, characterized in that the said reflux method in step (1), wherein, the liquid-solid ratio is 6-10, the extracting time at boiling condition is 1-2 h, the residue is repeatedly extracted for 1-2 times, and the filtrate is merged.
 5. Enrichment method of Ergosterol peroxide from sporoderm-broken Ganoderma lucidum spore powder according to claim 1, characterized in that the said step (2), wherein, the medium pressure preparative chromatography column is packed with 30-50 μm ODS silica gel, the height of column is 45 cm, the solid content of sample solution is 0.05-0.2 g/mL, the injection rate is 2-5 mL/min and the injection volume is 0.1 BV, performing isocratic elution with 60-95% methanol aqueous solution at the rate of 1.2-2.0 BV/h. 6-7. (canceled)
 8. Enrichment method of Ergosterol peroxide from sporoderm-broken Ganoderma lucidum spore powder according to claim 1, characterized in that the said step (3), wherein, the solid content of sample solution is 0.05-0.2 g/mL, the simulated moving-bed chromatography system uses ODS reversed silica gel with particle size of 30-50 μm as packing materials, the system, adopting 8-16 columns in series connection, is divided into four areas, each of which having 1-4 columns in series connection, the system parameters are set up as follows: room temperature, flow rate of injection pump is 3-6 mL/min, flow rate of elution pump is 16-38 mL/min, Extraction velocity is 10-23 mL/min, flow rate for raffinate is 9-21 mL/min, and switching time is 10-24 min.
 9. Enrichment method of Ergosterol peroxide from sporoderm-broken Ganoderma lucidum spore powder according to claim 2, characterized in that the said step (3), wherein, the solid content of sample solution is 0.05-0.2 g/mL, the simulated moving-bed chromatography system uses ODS reversed silica gel with particle size of 30-50 μm as packing materials, the system, adopting 8-16 columns in series connection, is divided into four areas, each of which having 1-4 columns in series connection, the system parameters are set up as follows: room temperature, flow rate of injection pump is 3-6 mL/min, flow rate of elution pump is 16-38 mL/min, Extraction velocity is 10-23 mL/min, flow rate for raffinate is 9-21 mL/min, and switching time is 10-24 min.
 10. Enrichment method of Ergosterol peroxide from sporoderm-broken Ganoderma lucidum spore powder according to claim 3, characterized in that the said step (3), wherein, the solid content of sample solution is 0.05-0.2 g/mL, the simulated moving-bed chromatography system uses ODS reversed silica gel with particle size of 30-50 μm as packing materials, the system, adopting 8-16 columns in series connection, is divided into four areas, each of which having 1-4 columns in series connection, the system parameters are set up as follows: room temperature, flow rate of injection pump is 3-6 mL/min, flow rate of elution pump is 16-38 mL/min, Extraction velocity is 10-23 mL/min, flow rate for raffinate is 9-21 mL/min, and switching time is 10-24 min.
 11. Enrichment method of Ergosterol peroxide from sporoderm-broken Ganoderma lucidum spore powder according to claim 4, characterized in that the said step (3), wherein, the solid content of sample solution is 0.05-0.2 g/mL, the simulated moving-bed chromatography system uses ODS reversed silica gel with particle size of 30-50 μm as packing materials, the system, adopting 8-16 columns in series connection, is divided into four areas, each of which having 1-4 columns in series connection, the system parameters are set up as follows: room temperature, flow rate of injection pump is 3-6 mL/min, flow rate of elution pump is 16-38 mL/min, Extraction velocity is 10-23 mL/min, flow rate for raffinate is 9-21 mL/min, and switching time is 10-24 min.
 12. Enrichment method of Ergosterol peroxide from sporoderm-broken Ganoderma lucidum spore powder according to claim 5, characterized in that the said step (3), wherein, the solid content of sample solution is 0.05-0.2 g/mL, the simulated moving-bed chromatography system uses ODS reversed silica gel with particle size of 30-50 μm as packing materials, the system, adopting 8-16 columns in series connection, is divided into four areas, each of which having 1-4 columns in series connection, the system parameters are set up as follows: room temperature, flow rate of injection pump is 3-6 mL/min, flow rate of elution pump is 16-38 mL/min, Extraction velocity is 10-23 mL/min, flow rate for raffinate is 9-21 mL/min, and switching time is 10-24 min.
 13. Enrichment method of Ergosterol peroxide from sporoderm-broken Ganoderma lucidum spore powder according to claim 1, characterized in that the said step (4), wherein, the dosage of ethyl acetate-cyclohexane is 10-20 times that of the dry extract C, the volume ratio of ethyl acetate to cyclohexane is 50:50-10:90, and the time of recrystallization is 36-48 h.
 14. Enrichment method of Ergosterol peroxide from sporoderm-broken Ganoderma lucidum spore powder according to claim 2, characterized in that the said step (4), wherein, the dosage of ethyl acetate-cyclohexane is 10-20 times that of the dry extract C, the volume ratio of ethyl acetate to cyclohexane is 50:50-10:90, and the time of recrystallization is 36-48 h.
 15. Enrichment method of Ergosterol peroxide from sporoderm-broken Ganoderma lucidum spore powder according to claim 3, characterized in that the said step (4), wherein, the dosage of ethyl acetate-cyclohexane is 10-20 times that of the dry extract C, the volume ratio of ethyl acetate to cyclohexane is 50:50-10:90, and the time of recrystallization is 36-48 h.
 16. Enrichment method of Ergosterol peroxide from sporoderm-broken Ganoderma lucidum spore powder according to claim 4, characterized in that the said step (4), wherein, the dosage of ethyl acetate-cyclohexane is 10-20 times that of the dry extract C, the volume ratio of ethyl acetate to cyclohexane is 50:50-10:90, and the time of recrystallization is 36-48 h.
 17. Enrichment method of Ergosterol peroxide from sporoderm-broken Ganoderma lucidum spore powder according to claim 5, characterized in that the said step (4), wherein, the dosage of ethyl acetate-cyclohexane is 10-20 times that of the dry extract C, the volume ratio of ethyl acetate to cyclohexane is 50:50-10:90, and the time of recrystallization is 36-48 h. 